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Journal Articles
Accepted Manuscript
Journal:
Journal of Fluids Engineering
Article Type: Research-Article
J. Fluids Eng.
Paper No: FE-22-1122
Published Online: May 25, 2022
Journal Articles
Accepted Manuscript
Journal:
Journal of Fluids Engineering
Article Type: Research-Article
J. Fluids Eng.
Paper No: FE-21-1448
Published Online: May 25, 2022
Journal Articles
Journal:
Journal of Fluids Engineering
Article Type: Research-Article
J. Fluids Eng. October 2022, 144(10): 101207.
Paper No: FE-22-1102
Published Online: May 19, 2022
Journal Articles
Journal:
Journal of Fluids Engineering
Article Type: Research-Article
J. Fluids Eng. October 2022, 144(10): 101204.
Paper No: FE-21-1623
Published Online: May 19, 2022
Journal Articles
Journal:
Journal of Fluids Engineering
Article Type: Research-Article
J. Fluids Eng. October 2022, 144(10): 101206.
Paper No: FE-22-1006
Published Online: May 19, 2022
Journal Articles
Journal:
Journal of Fluids Engineering
Article Type: Research-Article
J. Fluids Eng. October 2022, 144(10): 101205.
Paper No: FE-21-1689
Published Online: May 19, 2022
Journal Articles
Journal:
Journal of Fluids Engineering
Article Type: Research-Article
J. Fluids Eng. October 2022, 144(10): 101303.
Paper No: FE-22-1013
Published Online: May 19, 2022
Image
in Interfacial Characteristics of Power-Law Viscoelastic Fluid With Heat and Mass Transfer in Planar Configuration
> Journal of Fluids Engineering
Published Online: May 19, 2022
Fig. 1 The schematic diagram of the interface The schematic diagram of the interface More
Image
in Interfacial Characteristics of Power-Law Viscoelastic Fluid With Heat and Mass Transfer in Planar Configuration
> Journal of Fluids Engineering
Published Online: May 19, 2022
Fig. 2 Growth rate variation with power-law index n ( ρ = 0.001 , Q = 0.5 , Re = 50 , We = 100 , Re l = 100 , α = 0.03 ) Growth rate variation with power-law index n (ρ=0.001,Q=0.5,Re=50,We=100,Rel=100,α=0.03) More
Image
in Interfacial Characteristics of Power-Law Viscoelastic Fluid With Heat and Mass Transfer in Planar Configuration
> Journal of Fluids Engineering
Published Online: May 19, 2022
Fig. 3 Growth rate variation with impact factor Q ( ρ = 0.001 , Re = 50 , We = 100 , n = 0.8 , Re l = 100 , α = 0.03 ) Growth rate variation with impact factor Q (ρ=0.001,Re=50,We=100,n=0.8,Rel=100,α=0.03) More
Image
in Interfacial Characteristics of Power-Law Viscoelastic Fluid With Heat and Mass Transfer in Planar Configuration
> Journal of Fluids Engineering
Published Online: May 19, 2022
Fig. 4 Effect of Reynolds number Re ( ρ = 0.001 , Q = 0.5 , We = 100 , n = 0.8 , Re l = 100 , α = 0.03 ) Effect of Reynolds number Re (ρ=0.001,Q=0.5,We=100,n=0.8,Rel=100,α=0.03) More
Image
in Interfacial Characteristics of Power-Law Viscoelastic Fluid With Heat and Mass Transfer in Planar Configuration
> Journal of Fluids Engineering
Published Online: May 19, 2022
Fig. 5 Effect of normalized Reynolds number Re l ( ρ = 0.001 , Q = 0.5 , Re = 50 , W e = 100 , n = 0.8 , α = 0.03 ) Effect of normalized Reynolds number Rel (ρ=0.001,Q=0.5,Re=50,We=100,n=0.8,α=0.03) More
Image
in Interfacial Characteristics of Power-Law Viscoelastic Fluid With Heat and Mass Transfer in Planar Configuration
> Journal of Fluids Engineering
Published Online: May 19, 2022
Fig. 6 Heat transport effect on growth rate ( ρ = 0.001 , Q = 0.5 , Re = 50 , We = 100 , n = 0.8 , Re l = 100 ) Heat transport effect on growth rate (ρ=0.001,Q=0.5,Re=50,We=100,n=0.8,Rel=100) More
Image
in Interfacial Characteristics of Power-Law Viscoelastic Fluid With Heat and Mass Transfer in Planar Configuration
> Journal of Fluids Engineering
Published Online: May 19, 2022
Fig. 7 Weber number effect on growth rate ( ρ = 0.001 , Q = 0.5 , Re = 50 , n = 0.8 , Re l = 100 , α = 0.03 ) Weber number effect on growth rate (ρ=0.001,Q=0.5,Re=50,n=0.8,Rel=100,α=0.03) More
Image
in Interfacial Characteristics of Power-Law Viscoelastic Fluid With Heat and Mass Transfer in Planar Configuration
> Journal of Fluids Engineering
Published Online: May 19, 2022
Fig. 8 Growth rate for the various combination of the interface ( ρ = 0.001 , We = 100 , α = 0.03 ) Growth rate for the various combination of the interface (ρ=0.001,We=100,α=0.03) More
Image
in Local Entropy Generation Analysis for Cavitation Flow Within a Centrifugal Pump
> Journal of Fluids Engineering
Published Online: May 19, 2022
Fig. 1 Grid in computation domain Grid in computation domain More
Image
in Local Entropy Generation Analysis for Cavitation Flow Within a Centrifugal Pump
> Journal of Fluids Engineering
Published Online: May 19, 2022
Fig. 2 Centrifugal pump closed test rig Centrifugal pump closed test rig More
Image
in Local Entropy Generation Analysis for Cavitation Flow Within a Centrifugal Pump
> Journal of Fluids Engineering
Published Online: May 19, 2022
Fig. 3 Comparison of the head curve between numerical and experimental results Comparison of the head curve between numerical and experimental results More
Image
in Local Entropy Generation Analysis for Cavitation Flow Within a Centrifugal Pump
> Journal of Fluids Engineering
Published Online: May 19, 2022
Fig. 4 Comparison of vapor structure evolution between numerical and experimental results Comparison of vapor structure evolution between numerical and experimental results More
Image
in Local Entropy Generation Analysis for Cavitation Flow Within a Centrifugal Pump
> Journal of Fluids Engineering
Published Online: May 19, 2022
Fig. 5 Comparison of head losses obtained by the local entropy generation method, global entropy generation method, and pressure drop method Comparison of head losses obtained by the local entropy generation method, global entropy generation method, and pressure drop method More